JPS5896829A - Purifying method for metal - Google Patents

Purifying method for metal

Info

Publication number
JPS5896829A
JPS5896829A JP19658381A JP19658381A JPS5896829A JP S5896829 A JPS5896829 A JP S5896829A JP 19658381 A JP19658381 A JP 19658381A JP 19658381 A JP19658381 A JP 19658381A JP S5896829 A JPS5896829 A JP S5896829A
Authority
JP
Japan
Prior art keywords
metal
molten metal
rolls
molten
crystallized
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP19658381A
Other languages
Japanese (ja)
Other versions
JPH0147533B2 (en
Inventor
Tatsufumi Kurofuchi
黒淵 達史
Shiro Matsuoka
松岡 司郎
Minoru Inoue
実 井上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Light Metal Industries Ltd
Original Assignee
Mitsubishi Light Metal Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Light Metal Industries Ltd filed Critical Mitsubishi Light Metal Industries Ltd
Priority to JP19658381A priority Critical patent/JPS5896829A/en
Publication of JPS5896829A publication Critical patent/JPS5896829A/en
Publication of JPH0147533B2 publication Critical patent/JPH0147533B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To recover metal having high purity effectively by immersing the cooled surface for crystallization of metal into molten metal, and moving the same upward from the molten metal while pressurizing the metal crystallized on said surface with rotating rolls. CONSTITUTION:The lower parts of cooled horizontal rolls 2 of which a pair of opposed surfaces move and rotate upward are immersed in, for example, molten Al 1 which is controlled of temp. to the neighborhood of the liquidus line in a molten metal well 5. Purifed Al3 is crystallized on the lower surfaces of the rolls 2 and in the state of removing the purified Al upward from the molten metal 1 by the rotation of the rolls 2, the same is compressed by the pressure exerted between the rolls 2. The half molten part separated from the solid phase by the compression is returned into the molten metal. In order to prevent oxidation of the Al, etc. the surface of the metal 1 is preferably kept in an inert gaseous atmosphere of N2, etc. The strip-like purified Al removed upward from the metal 1 is cut with a shear 7 via pinch rolls 6 to a cut plate or is coiled with a coiler 8 to a product.

Description

【発明の詳細な説明】 本発明は金属の純化方法に関する。詳しくは本発明は不
純物を含有する金属から分別結晶法により高純度の板状
金属を得る方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying metals. Specifically, the present invention relates to a method for obtaining a highly pure plate metal from a metal containing impurities by a fractional crystallization method.

従来、金属の純化方法、特にアルミニウムの純化方法と
して各種の方法が提案され、その一部は既に工業的に採
用されている。例えば純度タデ、タッチ程度のアルミニ
ウムを得る方法として三層電解法及び分別晶析法が知ら
れており、又アルミニウムスクラップを純化する方法と
して回転晶析法、Zinkal (ツインカル)法、B
eck(ペック)法及び沈澱分離法等が提案されている
。しかしながら、これらの方法はいずれも経済的に有利
でなく、又純化効率が低い等の欠点を有するものもあり
、工業的に十分なものではなかった。
Conventionally, various methods have been proposed as methods for purifying metals, particularly for purifying aluminum, and some of them have already been adopted industrially. For example, the three-layer electrolytic method and the fractional crystallization method are known as methods for obtaining aluminum with a purity of about the same level as Tade, and the methods for purifying aluminum scrap include the rotational crystallization method, the Zinkal method, and the B
Eck (Peck) method, precipitation separation method, etc. have been proposed. However, none of these methods are economically advantageous, and some of them have drawbacks such as low purification efficiency, and are not industrially sufficient.

本発明者らはこれら従来法の欠点を解決し、工業的に有
利な金属の純化方法を見出すべく鋭意検討を重ねた結果
、分別晶析工程と機械的な圧搾工程とを組合せることに
より、極めて純度の高い金属を効率的に回収することが
できることを見い出して本発明に到達した。
The inventors of the present invention have made intensive studies to solve the drawbacks of these conventional methods and find an industrially advantageous metal purification method. As a result, by combining a fractional crystallization process and a mechanical squeezing process, The present invention was achieved by discovering that metals with extremely high purity can be efficiently recovered.

即ち本発明は、工業的に有利な金属の純化方法を提供す
ることを目的とし、この目的は液相線近傍に維持された
溶融金属中に冷却された金属晶析用表面を浸漬して該表
面上に金属を晶析させ、ついで金属の晶析した該表面を
回転するロールにより加圧しつつ溶融金属の上方に移動
させて晶析金属を圧搾しつつ回収することにより、容易
に達成される。
That is, an object of the present invention is to provide an industrially advantageous metal purification method, and the purpose is to immerse a cooled surface for metal crystallization into molten metal maintained near the liquidus line. This can be easily achieved by crystallizing the metal on a surface, then moving the crystallized surface above the molten metal while applying pressure with a rotating roll, and recovering the crystallized metal while squeezing it. .

以下に本発明をアルミニウムの純化に適用する場合に即
して詳細に説明する。
The present invention will be explained in detail below when applied to the purification of aluminum.

本発明においてはまず、液相線近傍に維持された溶融ア
ルミニウム中に、冷却された金属晶析用表面を浸漬して
該表面上にアルミニウムを晶析させる。このアルミニウ
ムの晶析工程においてはアルミニウムと共晶を構成する
元素、例えば鉄、マンガン、ケイ素、マグネシウム、亜
鉛、銅、ニッケル、ガリウム等の溶質成分を晶析時の溶
質分配作用を利用して初晶アルミニウムから分離する。
In the present invention, first, a cooled surface for metal crystallization is immersed in molten aluminum maintained near the liquidus line, and aluminum is crystallized on the surface. In this aluminum crystallization process, solute components such as elements that form a eutectic with aluminum, such as iron, manganese, silicon, magnesium, zinc, copper, nickel, and gallium, are first extracted using the solute distribution effect during crystallization. Separate from crystalline aluminum.

この際、分離効率(l−/。。)を高めるためには、C
BAco 、従って下記(2)式により算出されるke
を小さくする必要がある。4にって、晶析速度(R)及
び境界層厚さくd)を小さくすることが重要になる。
At this time, in order to increase the separation efficiency (l-/..), C
BAco, therefore ke calculated by the following formula (2)
needs to be made smaller. 4, it becomes important to reduce the crystallization rate (R) and the boundary layer thickness d).

−P′ にθ−1 %る。=ks(/ s)      ・・・・・・・・
・・・・・・・・・・(1)具体的には、晶析速度(R
)の制御は、アルミニウム溶湯からの除熱量が入熱量を
若干上回る程度にアルミニウム溶湯及び金属晶析用表面
の温度管理を行なうことにより達成される。晶析速度が
あまり小さくなると生産性に悪影響を与えるので、実操
作においては生産性と分離効率とを考慮して好適な範囲
に晶析速度を保つように制御する。境界層厚さくd)は
、固液界面の液相側、即ちアルミニウム溶湯の攪拌を充
分に行なうことにより減少させることができる。特に原
料として不純物濃度の高いアルミニウムスクラップを用
いる場合には、固液界面で局部的な成分の不均一状態を
生じ、得られるアルミニウムの純化度を低下させやすい
ので、特に効率的な溶湯の攪拌が望まれる。
-P' by θ-1%. =ks(/s)・・・・・・・・・
・・・・・・・・・・・・(1) Specifically, the crystallization rate (R
) is achieved by controlling the temperature of the molten aluminum and the surface for metal crystallization to such an extent that the amount of heat removed from the molten aluminum slightly exceeds the amount of heat input. If the crystallization rate becomes too low, productivity will be adversely affected, so in actual operation, the crystallization rate is controlled to be kept within a suitable range in consideration of productivity and separation efficiency. The boundary layer thickness d) can be reduced by sufficiently stirring the liquid phase side of the solid-liquid interface, that is, the molten aluminum. Particularly when aluminum scrap with a high concentration of impurities is used as a raw material, local non-uniformity of components occurs at the solid-liquid interface, which tends to reduce the purity of the resulting aluminum, so it is especially important to stir the molten metal efficiently. desired.

晶析工程で金属晶析用表面に晶析したアルミニウムを該
表面を回転するロールにより加圧しつつ溶融アルミニウ
ムの上方に移動させることによって圧搾する圧搾工程に
おいては、晶析したアルミニウムに機械的な圧力が加え
られることにより、更に純化度が高められる。即ち、通
常、本発明の晶析工程におけるような分別結晶化により
溶湯から分離された固相は純アルミニウムの他に幾分か
の不純物分(溶質成分)を含み、これがアルミニウムと
共晶を作り晶析時の晶析温度では半溶融の状態にある。
In the crystallization process, the aluminum crystallized on the surface for metal crystallization is pressed by rotating rolls and moved above the molten aluminum to compress it. By adding , the degree of purity is further increased. That is, normally, the solid phase separated from the molten metal by fractional crystallization as in the crystallization process of the present invention contains pure aluminum and some impurities (solute components), which form eutectic with aluminum. At the crystallization temperature during crystallization, it is in a semi-molten state.

そこでこの半溶融の共晶部分を機械的圧搾によシ固相分
から分離することによって得られるアルミニウムの純度
を高めるのである。
Therefore, the purity of the aluminum obtained is increased by separating this semi-molten eutectic portion from the solid phase by mechanical compression.

次に本発明を、本発明の実施態様の例を示す第1図〜第
ダ図を参照しながらさらに具体的に説明する。
Next, the present invention will be explained in more detail with reference to FIGS. 1 to 3, which show examples of embodiments of the present invention.

第1図は本発明の実施に好適な純化金属の回収装置の一
例を示す概略縦断面図である。第1図において、溶湯溜
め(5)中で液相線近傍に温度制御されたアルミニウム
溶湯(1)中に、一対の、対向する面が上向きに移動す
るような向きに回転する、冷却された水平ロール(2)
の下部を浸漬し、該ロールの下部表面に純化アルミニウ
ム(3)を晶析させる。水平ロール(コ)の冷却方法と
しては特に制限はなく、外部冷却方式又は内部冷却方式
等が採用し得る。例えば第2図(a)に示すように、水
平ロール(埒の上部表面に供給ノズル(/l)から冷却
気体を吹き付けて冷却する方法、第2図(b)に示すよ
うに、別に設けた冷却用ロール(/萄と接触させて冷却
する方法、又は第一図(C)に示すようにロール(2)
内部に冷却媒体導入管(/3)及び導出管(/りを設は
ロール内部に冷却気体又は冷却液体を供給して冷却する
方法等が挙げられる。
FIG. 1 is a schematic vertical sectional view showing an example of a purified metal recovery apparatus suitable for carrying out the present invention. In Fig. 1, a pair of cooled aluminum melts (1) whose temperature is controlled near the liquidus line in a molten metal reservoir (5) are rotated in such a direction that a pair of opposing surfaces move upward. Horizontal roll (2)
The lower part of the roll is immersed to crystallize purified aluminum (3) on the lower surface of the roll. There is no particular restriction on the method of cooling the horizontal roll (co), and an external cooling method, an internal cooling method, or the like may be adopted. For example, as shown in Fig. 2 (a), there is a method in which cooling gas is sprayed from a supply nozzle (/l) onto the upper surface of a horizontal roll (Fig. 2); A cooling roll (a method of cooling by bringing it into contact with the grapes, or a roll (2) as shown in Figure 1 (C))
Examples include a method of providing a cooling medium inlet pipe (/3) and an outlet pipe (/3) inside the roll and supplying cooling gas or cooling liquid to the inside of the roll for cooling.

水平ロール(コ)の表面に晶析した純化アルミニウム(
3ンは該ロールの回転によシ溶湯から上方に取り出され
る際に該ロール間に加えられる圧力により圧搾される。
Purified aluminum (
The three cylinders are squeezed by the pressure applied between the rolls as they are removed upward from the molten metal by rotation of the rolls.

ここで圧搾により固相から分離された半溶融部分は重力
による沈降又は濃度差による拡散により溶湯中に戻され
る。ロール(2)の回転速度は、溶湯成分、ロール径並
びに得ようとする板厚及びその純度等によって実験的又
は経験的に容易に決定される。″またロールの材質は特
に制限はないが、溶湯を汚染せず、熱伝導性が良く、且
つ耐熱性及び耐久性を有するものが望ましく、一般的に
は鋼又はカーボンライニングされた鋼が好適である。
Here, the semi-molten portion separated from the solid phase by compression is returned to the molten metal by sedimentation due to gravity or diffusion due to concentration difference. The rotational speed of the roll (2) is easily determined experimentally or empirically depending on the molten metal composition, the roll diameter, the desired plate thickness and its purity, etc. ``The material of the roll is not particularly limited, but it is desirable that it does not contaminate the molten metal, has good thermal conductivity, and has heat resistance and durability. Generally, steel or carbon-lined steel is suitable. be.

なお溶湯の表面は、アルミニウム又は含有される溶質成
分の酸化を防ぐために窒素又はアルゴン等の不活性ガス
雰囲気とすることが望ましい。また、溶湯の攪拌は必須
ではないが純化度を高めるためには攪拌することが望ま
しい。溶湯の攪拌方法としては第1図に示す如く、溶湯
中に挿入された攪拌羽根(り)を回転する方法の他、溶
湯溜め(夕)の下部から微細気泡を放出させる方法、電
磁力によって溶湯を回転させる方法、あるいはこれらの
方法を組合せた方法、等が挙げられる。溶湯から上方に
取り出されたロール間での圧搾を経た帯板状の純化アル
ミニウムは、ピンチロール(6)を経て、シャー(7)
により切断され切板とされるか、又は巻き取り機(めで
コイル状に巻き取られて製品とされる。
Note that the surface of the molten metal is preferably kept in an inert gas atmosphere such as nitrogen or argon in order to prevent oxidation of aluminum or the solute components contained therein. Furthermore, although stirring of the molten metal is not essential, it is desirable to stir the molten metal in order to increase the degree of purity. As shown in Figure 1, methods for stirring the molten metal include rotating a stirring blade inserted into the molten metal, releasing fine bubbles from the lower part of the molten metal reservoir, and stirring the molten metal using electromagnetic force. Examples include a method of rotating the object, or a method of combining these methods. The band-shaped purified aluminum that has been taken out upward from the molten metal and squeezed between rolls passes through pinch rolls (6) and then shears (7).
The product is either cut into a cut plate using a machine, or wound into a coil using a winding machine.

第3図は本発明の実施に好適な純化金属の回収装置の他
の例を示す概略縦断面図である。第3図(a)において
液相線近傍に温度制御されたアルミニウム溶湯(21)
中に冷却された板体(22)を浸漬し、該板体の表面に
純化アルミニウム(3)を晶析させる。板体(1)の冷
却方法としては特に制限はないが、例えば第り図に板体
の縦断回動媒体供給ノズル(3/)により冷却気体を一
給することにより冷却する方法等が挙げられる。なお冷
却媒体は気体に限られず、排出経路が確保されるならば
液体でもよい。
FIG. 3 is a schematic vertical sectional view showing another example of a purified metal recovery apparatus suitable for carrying out the present invention. In Figure 3(a), molten aluminum (21) whose temperature is controlled near the liquidus line
A cooled plate (22) is immersed therein, and purified aluminum (3) is crystallized on the surface of the plate. There are no particular restrictions on the method of cooling the plate (1), but examples include a method of cooling the plate by supplying cooling gas once through the longitudinally rotating medium supply nozzle (3/) of the plate, as shown in Figure 1. . Note that the cooling medium is not limited to gas, but may be liquid as long as a discharge path is secured.

板体(〃)の表面に晶析した純化アルミニウム(3)は
、第3図(b)に示す如く、該板体を上方に引き上げる
と同時に溶湯の上方に水平に設けられた一対の双向ロー
ル(2W)により加えられる圧力によって圧搾される。
The purified aluminum (3) that has crystallized on the surface of the plate (〃) is pulled upwards at the same time as the plate is pulled up by a pair of bidirectional rolls installed horizontally above the molten metal. It is squeezed by the pressure applied by (2W).

ロール(42g′)の形式は特に制限されないが、自動
回転式のロールが好ましい。ロール゛(2St)及び板
材(1)の材質は特に制限されないが、前述の第1図の
装置におけるロール(コ)の材質と同様の理由から、鋼
又はカーボンライニングされた鋼が好ましい。圧搾によ
り分離された半溶融部分は第1図における場合と同様に
溶湯中に戻される。
The type of roll (42g') is not particularly limited, but a self-rotating roll is preferred. The materials of the roll (2St) and the plate (1) are not particularly limited, but steel or carbon-lined steel is preferred for the same reason as the material of the roll (co) in the apparatus shown in FIG. 1 described above. The semi-molten portion separated by squeezing is returned to the molten metal as in FIG.

この場合においても、攪拌羽根(2り)等により溶湯を
攪拌すること、或は溶湯の表面を不活性ガス雰囲気とす
ることは純度の高い純化アルミニウムを得るために望ま
しいことである。
In this case as well, it is desirable to stir the molten metal using a stirring blade (two) or the like or to create an inert gas atmosphere on the surface of the molten metal in order to obtain purified aluminum with high purity.

このように冷却された板体を用いて板体表面に純化アル
ミニウムを晶析させる方法においては、晶析金属を回収
することなく板体の上昇・下降を繰り返すことにより、
純化アルミニウムの晶析と圧搾とを数回繰り返し、板体
表面に純化アルミニウムを多層晶析させて、生産性を向
上させることもできる。この場合にはロール(2W)の
間隔を純化アルミニウムの層厚に応じて制御することが
重要である。
In this method of crystallizing purified aluminum on the plate surface using a cooled plate, the plate is repeatedly raised and lowered without recovering the crystallized metal.
Productivity can also be improved by repeating crystallization and compression of purified aluminum several times to crystallize multiple layers of purified aluminum on the surface of the plate. In this case, it is important to control the interval between the rolls (2W) according to the layer thickness of purified aluminum.

溶湯から上方に取り出されたロール間での圧搾を経た板
状の純化アルミニウムは面前機を用される。
The plate-shaped purified aluminum that has been taken out upward from the molten metal and compressed between rolls is then used in a surface-forming machine.

本発明によれば、金属の晶析と圧搾とを効率的に組み合
せることにより純化金属を連続的又は半連続的に回収す
ることができ、生産性、作業性が優れており、従って経
済的にも極めて有利である。
According to the present invention, by efficiently combining metal crystallization and compression, purified metal can be recovered continuously or semi-continuously, and productivity and workability are excellent, so it is economical. It is also extremely advantageous.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施に適した純化金属の回収装置の一
例を示す概略縦断面図であり、第2図は第1図の装置の
水平ロールの冷却方法の例を示す図であり、第2図(a
)はロール表面に冷却気体を吹き付ける方法、第2図(
b)は別に設けた冷却用ロールを用いる方法、第2図(
C)はロール内部に冷却媒体を供給する方法を示す。 第3図は本発明の実施に適した純化金属の回収装置の他
の例を示す概略縦断面図であり、第3図(a)は板体を
溶湯に浸漬した状態を示し、第3図(b)は板体を溶湯
の上方に移動させる過程の状態を示す。第9図は第3図
の板材の冷却方法の例を示す縦断面図である。 図中、 /、2/・・・アルミニウム溶湯、コ・・・水平ロール
、3、+23・・・純化アルミニウム、り、25・・・
[t’羽m、g・・・ピンチロール、2・・・シャー、
!・・・巻き取り機、//・・・供給ノズル、/2・・
・冷却用ロール、/3・・・冷却媒体導入管、22・・
・板体、λり・・・ロール、3/・・・冷却媒体供給ノ
ズル。 第 2 凪 (c) (α)(?) 第4Σ
FIG. 1 is a schematic longitudinal sectional view showing an example of a purified metal recovery apparatus suitable for implementing the present invention, and FIG. 2 is a diagram showing an example of a method for cooling the horizontal roll of the apparatus of FIG. Figure 2 (a
) is a method of blowing cooling gas onto the roll surface, Figure 2 (
b) is a method using a separately provided cooling roll, as shown in Figure 2 (
C) shows a method of supplying a cooling medium inside the roll. FIG. 3 is a schematic vertical cross-sectional view showing another example of a purified metal recovery apparatus suitable for carrying out the present invention, and FIG. (b) shows the state in the process of moving the plate above the molten metal. FIG. 9 is a longitudinal sectional view showing an example of a method for cooling the plate material of FIG. 3. In the figure, /, 2/...molten aluminum, ko...horizontal roll, 3, +23...purified aluminum, ri, 25...
[t' wing m, g... pinch roll, 2... shear,
! ...winding machine, //...supply nozzle, /2...
・Cooling roll, /3...Cooling medium introduction pipe, 22...
・Plate body, λri...roll, 3/...cooling medium supply nozzle. 2nd Nagi (c) (α) (?) 4th Σ

Claims (1)

【特許請求の範囲】 (1)液相線近傍に維持された溶融金属中に冷却された
金属晶析用表面を浸漬して該表面上に金属を晶析させ、
ついで金属の晶析した該表面を回転するロールにより加
圧しつつ溶融金属の上方に移動させて晶析金属を圧搾し
つつ回収することを特徴とする金属の純化方法。 (2、特許請求の範囲第1項に記載の金属の純化方法に
おいて、対向面が上向きに移動するような向きに回転す
る一対の水平ロールの表面を金属晶析用表面として使用
し、該ロールの下部を溶融金属中に浸漬して、該ロール
の下部表面に晶析した金属晶析物を該ロール間に加えら
れる圧力により圧搾しつつ上方に移動させることを特徴
とする方法。 (3)特許請求の範囲第7項に記載の金属の純化方法に
おいて、板体の表面を金属晶析用表面として使用し、該
板体な溶融金属中に浸漬し次いて引き上げて、該板体の
表面に晶析した金属晶析物を溶融金属の上方に設けられ
たロールと該板体との間に加えられる圧力により圧搾し
つつ上方に移動させることを特徴とする方法。 (4)特許請求の範囲第7項ないし第3項のいずれか1
つに記載の金属の純化方法において、該溶融金属を攪拌
することを特徴とする方法。 (5)特許請求の範囲第1項ないし第り項のいずれか7
つに記載の金属の純化方法において、該溶融金属の表面
を不活性ガス雰囲気とすることを特徴とする方法。
[Claims] (1) A cooled metal crystallization surface is immersed in molten metal maintained near the liquidus line to crystallize the metal on the surface,
A method for purifying a metal, which comprises: then moving the surface of the crystallized metal above the molten metal while pressurizing it with a rotating roll, and recovering the crystallized metal while squeezing it. (2. In the metal purification method described in claim 1, the surfaces of a pair of horizontal rolls that rotate in such a direction that the opposing surfaces move upward are used as metal crystallization surfaces, and the rolls A method characterized by immersing the lower part of the roll in molten metal, and moving the metal crystallized substance crystallized on the lower surface of the roll upward while being squeezed by pressure applied between the rolls. (3) In the metal purification method according to claim 7, the surface of the plate is used as a surface for metal crystallization, and the plate is immersed in molten metal and then pulled up. A method characterized in that the metal crystallized material is moved upward while being squeezed by pressure applied between a roll provided above the molten metal and the plate. Any one of range 7 to 3
The method for purifying a metal according to item 1, which comprises stirring the molten metal. (5) Any one of claims 1 to 7
The method for purifying a metal according to item 1, characterized in that the surface of the molten metal is placed in an inert gas atmosphere.
JP19658381A 1981-12-07 1981-12-07 Purifying method for metal Granted JPS5896829A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19658381A JPS5896829A (en) 1981-12-07 1981-12-07 Purifying method for metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19658381A JPS5896829A (en) 1981-12-07 1981-12-07 Purifying method for metal

Publications (2)

Publication Number Publication Date
JPS5896829A true JPS5896829A (en) 1983-06-09
JPH0147533B2 JPH0147533B2 (en) 1989-10-16

Family

ID=16360150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19658381A Granted JPS5896829A (en) 1981-12-07 1981-12-07 Purifying method for metal

Country Status (1)

Country Link
JP (1) JPS5896829A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2564485A1 (en) * 1984-05-17 1985-11-22 Pechiney Aluminium PROCESS FOR THE CONTINUOUS PURIFICATION OF METALS BY FRACTIONAL CRYSTALLIZATION ON A ROTATING CYLINDER
JP2010031334A (en) * 2008-07-30 2010-02-12 Showa Denko Kk Method and apparatus for refining metal, refined metal, casting, metal product and electrolytic capacitor

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5020536A (en) * 1973-06-25 1975-03-04

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5020536A (en) * 1973-06-25 1975-03-04

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2564485A1 (en) * 1984-05-17 1985-11-22 Pechiney Aluminium PROCESS FOR THE CONTINUOUS PURIFICATION OF METALS BY FRACTIONAL CRYSTALLIZATION ON A ROTATING CYLINDER
JP2010031334A (en) * 2008-07-30 2010-02-12 Showa Denko Kk Method and apparatus for refining metal, refined metal, casting, metal product and electrolytic capacitor

Also Published As

Publication number Publication date
JPH0147533B2 (en) 1989-10-16

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